Flux in recovery of aluminum in reverberatory furnace

ABSTRACT

A process for the recovery of metal, particularly aluminum is disclosed whereby flux is in a ratio of less than about 0.4 flux to inert material in the dross.

This application is a continuation of Ser. No. 06/328605 now abandoned which-in-turn is a division of Ser. No. 06/192946, now abandoned.

This invention relates to an improved flux which can be used to process dross type materials in reverberatory furnaces to increase the metal recovered from these drosses.

BACKGROUND OF THE INVENTION

The secondary aluminum industry is concerned with the production of aluminum from slag, dross and scraps of a variety of origins generally unknown. Consequently, the constituents used in the secondary recovery furnaces contain impurities and oxides which must be separated during the melting process in order to segregate the valuable metal. It is important to have a flux which separates the metal from the scrap which includes a variety of dross, slag, recycled scrap, discarded cans and containers, salvaged castings and the like. Because of the nature of some of the scrap including its impurities, oxides and size of individual pieces, it becomes necessary to apply salt fluxes to minimize oxidation and improve slag formation during melting and thereby enhance the recovery rate of the valuable metal.

In particular, the dross type scrap which is produced by the primary aluminum companies and which is made by dry skimming the waste made in remelting furnaces represents one of the most valuable and yet most difficult types of material to process in the secondary aluminum industry.

The primary components of the dross are a plurality of aluminum oxides, hydrated aluminum oxides and entrained metallic aluminum plus small amounts of magnesium chloride, aluminum carbide, aluminum nitride and small percentages of calcium, silicon, magnesium, iron, zinc and manganese.

Because of the nature of the dross material which normally contains a sizeable fraction of non-metallic materials, several different types of secondary melting furnaces have been developed to process different types of scraps. In general, two types of furnaces are used to process scrap aluminum wastes. These are the rotary furnace and the reverberatory furnace. Both furnaces are suitable for processing all types of aluminum scraps, however, for individual specific scraps, one furnace may have advantages in its ability to recover metallic aluminum from the specific charge material.

Thus, for example, the rotary furnace may be shown to recover higher values of metal from low quality scraps such as drosses when these same drosses are processed by the reverberatory furnace; it does so, however, with the proviso that it is operated less economically because of the need for high quantities of flux salt and because of the inherent problems associated with the production of large quantities of salt containing waste products.

On the other hand, the reverberatory furnace can process the same dross material and produce lower quantities of waste product and recovered metal more economically, but it does so only at the expense of reduced metal recovery.

Thus there exists in the secondary aluminum recovery business a need for a flux or flux and process combination which would provide the highly efficient metal recovery of the rotary furnace while at the same time would produce this high recovery in the reverberatory furnace to take advantage of this type of furnace's economic advantages.

The quantities and compositions of fluxes used in the secondary industry depend very much on the particular plant, the operating practice, and the type of feed material used by numerous companies.

Generally, all rotary type furnaces employ chloride fluxes either as pure NaCl or as a physical mixture of NaCl and KCl. Furthermore, for rotary furnaces, it is customary to charge the salt flux into an empty furnace, melt the salt and then charge the scrap into the molten melt. This is particularly true for mixtures of NaCl and KCl. The advantage of this process is that it provides a flux which has a significant fluidity which acts like water. This fluidity depends on the composition, temperature and concentration ratio of the flux to the inert ingredients in the charge material. In order to take advantage of this fluidity, it is essential that the concentration ratio of flux to inert ingredients be greater than one (1) and that more flux than inert ingredients in the charge be used since too little flux leads to poor metal recovery. Unfortunately, because of the inherent design of reverberatory furnaces which utilize skim eye doors for the effective transfer of thermal energy to open charge wells, the flux mixture, usually 50% NaCl and 50% KCl, cannot be charged and melted on the well first since the liquid runs under and around the skim eye doors where it comes in contact with the high temperatures in the combustion box of the furnace and becomes superheated which causes flux loss by evaporation, wastes energy and creates a serious pollution problem.

Furthermore, the flux in a ratio greater than 1 flux to 1 inert oxide cannot be added after the charge has been placed on the reverberatory furnace well because on melting, the same problems exist as if it had been introduced initially.

To overcome this problem, fluxes of the NaCl and/or NaCl/KCl salts are normally used in reverberatory furnaces at a ratio of 0.6 to 0.8 flux to inert ingredient.

Using the flux with the above composition ratio leads to the production of a very viscous pastey slag which contains a high proportion of oxides and which can be physically removed from the furnace. However, this slag unfortunately contains a large quantity of metal which is not recovered in the furnace.

OBJECTS OF THE INVENTION

It is a primary object of the present invention to improve the process of the recovery of metal from dross in reverberatory furnaces.

It is a further object of this invention to combine the advantages ascribed to rotary furnaces for processing dross types of materials with the economic advantages of processing these same materials in a reverberatory furnace and to thus provide high metallic recovery from material processed in reverberatory furnaces.

It is a further object of this invention to provide an alloyed salt composition on the open charge well of a reverberatory furnace to enhance metal recovery from dross material which is substantially higher than the metal recovery presently obtained.

It is a further object of this invention to provide a pre-alloyed composition of NaCl and KCl salts as a flux for processing materials such as drosses which is used in quantities substantially lower than the quantities used in rotary furnaces and in reverberatory furnaces.

It is a further object of this invention to provide means of processing low metallic containing dross types of materials with an alloyed salt mixture on the charge well of a reverberatory furnace to provide substantially higher metallic recovery of the metal values of dross material while at the same time producing an innocuous furnace skim waste product which can be easily removed to land fill without serious consequence.

It is a further object of this invention to enhance recovery of metal value from dross materials while simultaneously reducing the total volume of flux used on the reverberatory furnace to produce a slag waste product containing a low concentration of chloride salts.

The above objects as well as others are accomplished generally speaking by using as a flux an alloyed mixture of salt and potash in the form of solid solution thereby improving significantly the metal recovered in a reverberatory furnace.

DESCRIPTION OF DRAWING

FIG. 1 is a composition diagram for mixtures of NaCl and KCl salts with temperature vs. weight by percent according to the present invention.

DESCRIPTION OF A PREFERRED EMBODIMENT

It will be appreciated from FIG. 1 that the individual chemical compounds NaCl and KCl are crystalline in nature and have a melting point of 1472° F. and 1454° F., respectively. In FIG. 1 X defines a liquidous boundary for the composition according to the weight by percent defined by the abscissa. Also Y defines a solidous boundary for the composition according to the weight by percent defined by the abscissa. Thus the area between X and Y define a partly liquid partly solid composition. As also shown in FIG. 1 with mixtures ranging from 40 percent NaCl and 60 percent KCl to 60 percent NaCl and 40 percent KCl, a solid solution mixture having a melting point at approximately 1225° F. is produced. In accordance with the present invention the two salts are alloyed together to yield a solid solution having the relatively lower melting point. In the absence of integral contact of alloyed salts, when sodium and potassium salts are charged into the bath, temperatures greater than their individual melting points are required to yield a solid solution compound. Thus, the addition of an alloyed salt of about equal parts of NaCl and KCl by weight results in the immediate availability of the relatively low melting point mixture used for fluxing of metallic aluminum in drosses. It will be appreciated as in many salt-potash mixtures, the use of fluoride salts or amount of cryolite to the solid solution salt improves the recovery of metal over that obtained when the salt potash flux alone is used.

In carrying out the preferred embodiment, the two salts used must be weighted proportionately in about equal parts to provide for a suitable mechanical mixture. As shown by FIG. 1 the mixtures can range from 40 to 60 percent by weight each of NaCl and KCl to produce the intended result. After mixing, it is necessary to preheat the salt mixture to produce a liquid which then provides for complete alloying and chemical intermixing of the mechanically mixed salts. To this can be added a small concentration of cryolite of about less than 3 percent by weight to improve recovery of metal.

After alloying of the salt mixture takes place, the material is poured from the thermal furnace and allowed to cool to room temperature. Subsequent to cooling, the solid solution salts are then processed in a hammer mill or grinding mill to produce particles of solid solution salt which can be used as a flux. These particles will, of course, vary in size but for our teaching, it is believed that they should be no larger than 3/4 inch and should pass at a minimum through a 3/4 inch mesh screen.

Upon completion of the above treatments, the thermally prepared solid solution of NaCl-KCl has been found to provide an extremely active flux which can be used in low concentrations on the charge well of reverberatory furnaces to process dross type materials and attain metal recovery from these dross materials at levels comparable with rotary furnaces while simultaneously providing a dry slag skim on the furnace well which can be easily removed by the reverberatory furnace operator.

The optimum metallic recovery from dross type materials is obtained when the above described thermally prepared flux is used in a concentration ratio of 0.3 to 0.4 flux to inert ingredient. Because of the lower melting point of thermally prepared solid solution flux mixture, the flux has better dispersion ability within the dross charge on the furnace well, resulting in highly improved metallic recovery in the reverberatory furnace. 

What is claimed is:
 1. A process for the recovery of metal from dross in a charge well of a reverberatory furnace wherein said dross includes at least one inert material and wherein the improvement comprises supplying thermally formed flux in solid particle form to the charge well in a ratio of thermally formed flux to said inert material of less than about 0.4, said flux being an alloyed mixture consisting essentially of a double salt which is 40% to 60% sodium chloride and 60% to 40% potassium chloride, said alloyed mixture having been produced by mechanically mixing said sodium chloride and said potassium chloride, heating the mixture to produce a liquid to effect complete alloying and chemical mixing thereof, and cooling the mixture to solidify it.
 2. A process according to claim 1 wherein said alloyed mixture has a melting point of about 1225° F.
 3. A process according to claim 1 wherein said flux further includes a fluoride salt in an amount less than 10 percent by weight.
 4. A process for the recovery of aluminum from dross wherein a flux layer is used over a pool of melted aluminum, and including at least one inert material in a charge well of a reverberatory furnace, said flux being introduced into the charge well as solid flux particles, the improvement wherein the composition of said flux particles consists essentially of an alloyed mixture which is 40% to 60% sodium chloride and 60% to 40% potassium chloride, and cryolite in an amount less than three percent by weight, said alloyed mixture having been produced by mechanically mixing said sodium chloride, said potassium chloride, and said cryolite, heating the mixture to produce a liquid to effect complete alloying and chemical mixing thereof, and cooling the mixture to solidify it, said solid flux particles and said dross being supplied to said charge well in a ratio of flux to said inert material in said dross of less than about 0.4, and being heated in the charge well to a melting point to effect proper dispersion of said flux within said dross at about 1225° F.
 5. A process according to claim 4 wherein the recovery of aluminum from dross is accomplished at a level comparable with a rotary type furnace while the amount of flux used is substantially reduced.
 6. A process according to claim 4 wherein dry slag skim remaining on the well is an innocuous waste product that can be easily removed by the reverberatory furnace operator. 